JPH0330690B2 - - Google Patents

Info

Publication number
JPH0330690B2
JPH0330690B2 JP60064619A JP6461985A JPH0330690B2 JP H0330690 B2 JPH0330690 B2 JP H0330690B2 JP 60064619 A JP60064619 A JP 60064619A JP 6461985 A JP6461985 A JP 6461985A JP H0330690 B2 JPH0330690 B2 JP H0330690B2
Authority
JP
Japan
Prior art keywords
bottom wall
opening
periphery
plate
heat exchange
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP60064619A
Other languages
Japanese (ja)
Other versions
JPS61223213A (en
Inventor
Akizuna Nakagaki
Takeji Yoko
Akio Myazawa
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
TSUCHA SEISAKUSHO KK
Original Assignee
TSUCHA SEISAKUSHO KK
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by TSUCHA SEISAKUSHO KK filed Critical TSUCHA SEISAKUSHO KK
Priority to JP6461985A priority Critical patent/JPS61223213A/en
Priority to US06/834,816 priority patent/US4708199A/en
Publication of JPS61223213A publication Critical patent/JPS61223213A/en
Publication of JPH0330690B2 publication Critical patent/JPH0330690B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D9/00Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0012Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the apparatus having an annular form

Description

【発明の詳細な説明】 (産業上の利用分野) この発明は内燃機関用オイルクーラなどの熱交
換器の熱交換コアに関する。
DETAILED DESCRIPTION OF THE INVENTION (Field of Industrial Application) This invention relates to a heat exchange core for a heat exchanger such as an oil cooler for an internal combustion engine.

(従来の技術) 従来内燃機関用オイルクーラなどに、取付用の
ボルトを挿通するための中央口を設けた環形の多
板式のものが知られている。例えば特公昭55−
48238号に開示されている。その1例を第10図
に示す。オイルクーラ30は冷却水入口パイプ3
2、冷却水出口パイプ33を備えた筒形のケーシ
ング31の内部へクーラコア34を収容しオイル
入口35、オイル出口36に連通させたものであ
る。クーラコア34は、フイン37を収容しカラ
ー38で中央口と区画したクーラユニツト39と
間隔板40とを交互に積み重ねている。
(Prior Art) Conventionally, an annular multi-plate type oil cooler for an internal combustion engine is known, which has a central opening through which a mounting bolt is inserted. For example, special public service in 1977-
Disclosed in No. 48238. An example is shown in FIG. The oil cooler 30 is the cooling water inlet pipe 3
2. A cooler core 34 is housed inside a cylindrical casing 31 equipped with a cooling water outlet pipe 33 and communicated with an oil inlet 35 and an oil outlet 36. The cooler core 34 has a cooler unit 39 that accommodates fins 37 and is separated from a center opening by a collar 38, and spacer plates 40 stacked alternately.

上記の熱交換器はクーラコアに間隔板を必要と
し、さらにケーシングを必要とするので大型で重
量大となり、部品点数も多い。そこで実公昭59−
28219号に開示されたオイルクーラのようなケー
シングを用いない積層形のものが提案されてい
る。このオイルクーラは、上下1対をなす上側板
と下側板を組み合わせ、さらにこれを所要段数重
ね合わせたうえ、その下面に下端板、上面にオイ
ル流出室となるリング状部材および冷却水の入
口、出口パイプを取付けたものである。この上側
板、下側板はそれぞれの底壁が段差をなして段差
部、凸部等が設けられている。この上側板、下側
板を組み合わせさらにこれを重ね合わせると、底
壁に設けた段差のある凸部や段差部の〓間が流体
の流路となる。また底壁に設けた上下方向の突出
部分を互に突き合わせ当接させ、その立上り部分
が2流体の境界をなし、突き合わせ面が上下の同
種流体の接触面となる。
The above-mentioned heat exchanger requires a spacer plate in the cooler core, and also requires a casing, so it is large and heavy, and has a large number of parts. Therefore, in 1983,
A laminated type oil cooler that does not use a casing, such as the oil cooler disclosed in No. 28219, has been proposed. This oil cooler combines a pair of upper and lower plates, which are stacked in a required number of stages, and has a lower end plate on the lower surface, a ring-shaped member serving as an oil outflow chamber on the upper surface, and a cooling water inlet. It has an outlet pipe attached. The bottom walls of the upper and lower plates each form a step, and are provided with a stepped portion, a convex portion, and the like. When the upper plate and the lower plate are combined and stacked on top of each other, the stepped convex portions provided on the bottom wall and the spaces between the stepped portions become fluid flow paths. Further, the vertically protruding portions provided on the bottom wall are brought into contact with each other, and the rising portion forms a boundary between the two fluids, and the abutting surface becomes a contact surface between the upper and lower similar fluids.

(発明が解決しようとする課題) 上記のような熱交換器において、前者のものは
ケーシングを要し部品点数も多く、大形重量大か
つ組立て工数大などの問題がある。後者のものは
上側板、下側板2種のものを1組とすることが必
要であり、両者おのおのの底壁に段差を付して段
差部や凸部などを設けねばならない。このような
上側板、下側板は通常金属板のプレス成形によつ
て製作されるから、上記のような段差部や凸部な
どを正確に段差を付し、それぞれが平坦で反りが
ないように成形するのは困難である。従つて重ね
合わせたとき密着すべき部分に〓間を生じてろう
着不良による洩れを生じたり、流路形状が不正確
になつて所期以上に流体の圧力損失が大きくなつ
たりする。さらに底壁を突出させて突き合わせ当
接させた部分は同種流体間の接触面となるから当
接する面積だけ底壁の伝熱面積が減殺される。
(Problems to be Solved by the Invention) Among the heat exchangers as described above, the former requires a casing, has a large number of parts, is large and heavy, and requires a large number of assembly steps. The latter requires a set of two types of upper and lower plates, and the bottom wall of each must be stepped to provide a stepped portion or a convex portion. These upper and lower plates are usually manufactured by press-forming metal plates, so the steps and protrusions mentioned above must be accurately stepped to ensure that they are flat and free of warping. Difficult to mold. Therefore, when they are overlapped, gaps may occur in the portions that should be in close contact, resulting in leaks due to poor soldering, or the shape of the flow path may become inaccurate, resulting in greater fluid pressure loss than expected. Furthermore, the portion where the bottom wall protrudes and abuts becomes a contact surface between fluids of the same type, so the heat transfer area of the bottom wall is reduced by the area of contact.

(課題を解決するための手段) この発明では底壁に段差のない単一プレートを
用い、これを円周方向にずらせて重ねることによ
り、2流体の流路が区分される熱交換コアを形成
させるものである。すなわち底壁の周縁と底壁中
央の中央口の周縁とに立上りフランジを設け、底
壁の同心円上に偶数個の開口を等ピツチで設けて
その一つおきに開口フランジを設けてプレートと
し、このプレートを1ピツチずつずらせて重ね合
わせて、交互に層状をなす第1・第2流路を形成
させ、これらプレートの上下端に上・下端板を固
着し、上・下端板のいずれかに、第1流路に連通
する第1流入口、第1流出口および第2流路に連
通する第2流入口、第2流出口を設けてなる熱交
換器の熱交換コアである。
(Means for Solving the Problems) In this invention, a single plate with no steps is used on the bottom wall, and by overlapping these plates with displacement in the circumferential direction, a heat exchange core is formed in which the flow paths of two fluids are divided. It is something that makes you That is, upright flanges are provided on the periphery of the bottom wall and the periphery of the central opening in the center of the bottom wall, and an even number of openings are provided on the concentric circle of the bottom wall at equal pitches, and an opening flange is provided every other opening to form a plate, These plates are stacked one on top of the other, shifted one pitch at a time, to form alternately layered first and second channels, and upper and lower end plates are fixed to the upper and lower ends of these plates, and either of the upper or lower end plates is , a heat exchange core of a heat exchanger including a first inlet and a first outlet communicating with the first flow path, and a second inlet and a second outlet communicating with the second flow path.

(作 用) この熱交換コアに、上端板、下端板に設けられ
た第1・第2流体の流入口、流出口に連通する入
口室、出口室、または入口パイプ、出口パイプが
取付けられて熱交換器を形成する。2流体はこれ
らの入口室または入口パイプから流入し1層おき
の流路に分流して流入し、再び各層の分流が集合
し、この間に底壁を介して各層毎に熱交換を行な
い流出口から流出する。
(Function) An inlet chamber, an outlet chamber, an inlet pipe, an outlet pipe, which communicate with the first and second fluid inlets and outlets provided in the upper end plate and the lower end plate, are attached to this heat exchange core. Form a heat exchanger. The two fluids flow in from these inlet chambers or inlet pipes, branch into flow channels every other layer, and the branched flows of each layer come together again. During this time, heat exchange is performed for each layer via the bottom wall, and the flow passes through the outlet. flows out from.

この熱交換コアのプレートは単一の形状のもの
を重ね合わせるのみであるから、構造が簡単で作
製容易である。またプレートの底壁は段付状の凹
凸を設けないでよいから反りがなく平坦に仕上げ
ることができ、重ね合わせたときの各フランジの
接合状態が良好で〓間を生じさせない。また底壁
は開口部分を除き全面積が上下各層の2流体の境
界面となり伝熱面として作用する。
Since the plates of this heat exchange core are made by simply overlapping plates of a single shape, the structure is simple and easy to manufacture. Further, since the bottom wall of the plate does not need to be provided with stepped irregularities, it can be finished flat without warping, and when stacked, the flanges are in a good joint state and do not create gaps. In addition, the entire area of the bottom wall, excluding the opening, serves as an interface between the two fluids in the upper and lower layers, and acts as a heat transfer surface.

(実施例) 第1図〜第4図によつて実施例を説明する。第
1図、第2図はこの発明の熱交換コア25(第3
図、第4図)を構成するプレート2である。プレ
ート2は、中央に中央口3を有する円形の平坦な
底壁5の周縁に立上りフランジ4b、中央口3の
周縁に立上りフランジ4aを設けてある。中央口
3と同心の円7上に開口6が45゜ずつの等分ピツ
チPで8個穿設されている。開口6は開口フラン
ジ8を周縁に設けた開口6aと、開口フランジを
設けない開口6bとが交互に配列されている。プ
レート2を伏せた姿勢で45゜ずつピツチをずらせ
て所要枚数だけ重ね合わせ、立上りフランジ4a
同士、4b同士を接合し、開口フランジ8を開口
6bの周縁に接合させる。こうすれば、上下方向
に配列される開口フランジ8の列によつて各底壁
5間に形成される層状の空室が1層おきに連通さ
れて、第1流入通路10、第1流出通路11を有
する第1流路(第3図)および第2流入通路1
2、第2流出通13を有する第2流路(第4図)
が形成される。この例では第1、第2流入通路、
第1・第2流出通路はいずれも2本ずつ形成され
る。このように重ね合わされたプレート2に上端
面に中央口9b、第1流出通路11に対向する第
1流出口9aを有する上端板9が固着され、また
これらのプレート2の下端面に中央口15a、第
1流入口15b、第2流入口15c、第2流出口
15dを有する下端板15が固着されて熱交換コ
ア25をなす。第3図、第4図に示す例では下端
板15の周縁に筒状垂下部15eが設けられてお
り、その内側に下蓋21が重ねられ筒状垂下部1
5eとの間に第2流体入口室17、第2流体出口
室18が形成される。入口パイプ19、出口パイ
プ20が前記第2流体の入口室・出口室に取付け
られ、第2流入口15c、第2流出口15dに連
通する。下蓋21の下面は第1流体入口室16を
形成し、第1流入口15bに連通する。上端板9
の上面には開口14aを有するリング状の上部室
14が取付けられ、その内部は第1流体出口室を
なして第1流出口9aに連通する。このようにし
てなる熱交換器1は第1流体をオイル、第2流体
を冷却水としたオイルクーラである。
(Example) An example will be described with reference to FIGS. 1 to 4. FIGS. 1 and 2 show the heat exchange core 25 (third part) of the present invention.
4). The plate 2 is provided with a rising flange 4b on the periphery of a circular flat bottom wall 5 having a central opening 3 in the center, and a rising flange 4a on the periphery of the central opening 3. Eight openings 6 are bored on a circle 7 concentric with the central opening 3 at equal pitches P of 45° each. The openings 6 have openings 6a provided with an opening flange 8 on the periphery and openings 6b without an opening flange arranged alternately. With the plates 2 in a face down position, shift the pitch by 45 degrees and overlap the required number of plates to form the rising flange 4a.
4b are joined to each other, and the opening flange 8 is joined to the periphery of the opening 6b. In this way, the layered cavities formed between the bottom walls 5 by the rows of opening flanges 8 arranged in the vertical direction are communicated every other layer, and the first inflow passage 10 and the first outflow passage are connected to each other. 11 (FIG. 3) and a second inflow channel 1
2. Second flow path with second outflow passage 13 (Fig. 4)
is formed. In this example, first and second inflow passages,
Two first and second outflow passages are formed. An upper end plate 9 having a central opening 9b on the upper end face and a first outlet 9a facing the first outflow passage 11 is fixed to the plates 2 stacked in this way, and a central opening 15a on the lower end face of these plates 2. , a lower end plate 15 having a first inlet 15b, a second inlet 15c, and a second outlet 15d is fixed to form a heat exchange core 25. In the example shown in FIGS. 3 and 4, a cylindrical hanging part 15e is provided on the periphery of the lower end plate 15, and a lower lid 21 is stacked on the inside of the cylindrical hanging part 15e.
5e, a second fluid inlet chamber 17 and a second fluid outlet chamber 18 are formed. An inlet pipe 19 and an outlet pipe 20 are attached to the inlet and outlet chambers of the second fluid, and communicate with the second inlet 15c and the second outlet 15d. The lower surface of the lower lid 21 forms the first fluid inlet chamber 16 and communicates with the first inlet 15b. Upper end plate 9
A ring-shaped upper chamber 14 having an opening 14a is attached to the upper surface of the chamber, and the inside thereof forms a first fluid outlet chamber and communicates with the first outlet 9a. The heat exchanger 1 thus constructed is an oil cooler in which the first fluid is oil and the second fluid is cooling water.

第5図第6図にプレートの他の例を示す。プレ
ート32は中央口を有する底壁35に開口36
a,36bが交互に90゜ピツチで中央口と同心の
円上に配列されている。開口36aには開口フラ
ンジ38を設け、開口36bには開口フランジを
設けない。また底壁35には突起37が複数個設
けられる。図示の90゜ピツチ領域P1と隣接の90゜ピ
ツチ領域P2とでは突起37の位置が対応しない
ように配列してある。プレート32を1ピツチ
90゜ずつずらせて重ね合わせると、P1領域の突起
37とP2領域の突起37とは重複することなく
隣接するプレート32の底壁35に当接する。突
起37は当該空室内の開口36b,36b間を流
れる流体に乱流を起こさせて熱交換効率を向上さ
せる。また各底壁35間の間隔を保つ支柱として
作用し高圧流体に対し耐圧力が増加する。プレー
ト32を重ね合わせて構成した熱交換コアの縦断
面は第3図、第4図と同様のものとなる。
Other examples of plates are shown in FIGS. 5 and 6. The plate 32 has an opening 36 in the bottom wall 35 with a central opening.
A and 36b are arranged alternately at a 90° pitch on a circle concentric with the center opening. The opening 36a is provided with an opening flange 38, and the opening 36b is not provided with an opening flange. Further, a plurality of protrusions 37 are provided on the bottom wall 35. The projections 37 are arranged so that the positions of the illustrated 90° pitch region P 1 and the adjacent 90° pitch region P 2 do not correspond. 1 pitch of plate 32
When they are shifted by 90 degrees and overlapped, the protrusions 37 in the P 1 area and the protrusions 37 in the P 2 area abut against the bottom wall 35 of the adjacent plate 32 without overlapping. The protrusion 37 causes turbulence in the fluid flowing between the openings 36b, 36b in the cavity, thereby improving heat exchange efficiency. In addition, it acts as a support to maintain the distance between the bottom walls 35, increasing the pressure resistance against high-pressure fluid. The longitudinal section of the heat exchange core constructed by overlapping the plates 32 is similar to that shown in FIGS. 3 and 4.

第7図、第8図にさらに他のプレートの例を示
す。介して42は2個の同心円47a,47b上
に開口45a,45bおよび46a,46bが
180゜ピツチで設けられ、45a,46aには開口
フランジが設けられる。開口45a,45b,4
6a,46bは同一直径上に配設される。また複
数の突起37が180゜ピツチで互に対応しない位置
に設けられる。プレート42を1ピツチ180゜ずつ
ずらせて重ね合わせ第3図、第4図と同様に上端
板、下端板を固着すると、第9図に断面で示す本
発明の熱交換コアが得られる。第9図はこの熱交
換コアを用いた熱交換器41である。プレート3
2を用いた熱交換コアは第9図に図示されるよう
に第1流入通路、第1流出通路、第2流入通路、
第2流出通路が同一縦断面上に現われ、各層の空
室内で流体は開口45b・46b間を、左右に分
かれてほぼ半周するように流れる。
Further examples of other plates are shown in FIGS. 7 and 8. 42 has openings 45a, 45b and 46a, 46b on two concentric circles 47a, 47b.
They are provided at a pitch of 180°, and opening flanges are provided at 45a and 46a. Openings 45a, 45b, 4
6a and 46b are arranged on the same diameter. Further, a plurality of protrusions 37 are provided at positions that do not correspond to each other at a pitch of 180°. When the plates 42 are stacked one on top of the other with a 180° offset by one pitch and the upper and lower end plates are fixed in the same manner as in FIGS. 3 and 4, the heat exchange core of the present invention shown in cross section in FIG. 9 is obtained. FIG. 9 shows a heat exchanger 41 using this heat exchange core. plate 3
As shown in FIG. 9, the heat exchange core using 2 has a first inflow passage, a first outflow passage, a second inflow passage,
A second outflow passage appears on the same longitudinal section, and the fluid flows approximately half a circle between the openings 45b and 46b in the cavities of each layer, dividing into left and right sides.

(発明の効果) この発明の熱交換コアは単一のプレートを重ね
合わせて上下端板を固着する構成であり、プレー
トは底壁が平坦で段付状の凹凸がないから構造簡
単で作成容易である。そしてプレートの底壁が平
坦で形状が単純であるから、正確な寸法のものが
得られ、立上りフランジや開口、フランジを接合
させたときの密着が完全である。従つてろう付け
洩れ等がなく機能が保証された熱交換器が得られ
る。またプレートの底壁は開口部分を除き全面積
が伝熱面となるから熱交換効率がよく、小型化で
き、構造簡単であり部品点数が少ないこと相まつ
て軽量化されたものとなる効果がある。またプレ
ートの積層数を増やして伝熱面積を増加させる
と、流体流路が長くならず流路断面積が増えるか
ら、圧力損失は減少するという有利な構造であ
る。
(Effects of the Invention) The heat exchange core of this invention has a structure in which a single plate is superimposed and the upper and lower end plates are fixed, and the plate has a flat bottom wall and no stepped irregularities, so the structure is simple and easy to manufacture. It is. Furthermore, since the bottom wall of the plate is flat and the shape is simple, accurate dimensions can be obtained, and the upright flanges, openings, and flanges will have perfect adhesion when joined. Therefore, a heat exchanger with guaranteed functionality without brazing leakage etc. can be obtained. In addition, since the entire area of the bottom wall of the plate, excluding the opening, is a heat transfer surface, it has good heat exchange efficiency, can be made compact, has a simple structure, has a small number of parts, and has the effect of being lightweight. . Furthermore, if the heat transfer area is increased by increasing the number of laminated plates, the fluid flow path will not become longer and the cross-sectional area of the flow path will increase, which is an advantageous structure in that pressure loss will be reduced.

【図面の簡単な説明】[Brief explanation of drawings]

第1図はこの発明のプレートの平面図、第2図
は第1図−線の断面図、第3図、第4図は実
施例を示す断面図、第5図は他のプレートの平面
図、第6図イ,ロは第5図イ−イ、ロ−ロ線の断
面図である。第7図はさらに他のプレートの平面
図、第8図イ,ロは第7図イ−イ線、ロ−ロ線の
断面図、第9図は第7図のプレートを用いた熱交
換コアを示す断面図、第10図は従来の熱交換器
を示す断面図である。 2,32,42……プレート、4a,4b……
立上りフランジ、5,35……底壁、6,6a,
6b,36a,36b,46a,46b……開
口、8,38……開口フランジ、9……上端板、
15……下端板、37……突起。
Fig. 1 is a plan view of the plate of the present invention, Fig. 2 is a sectional view along the line of Fig. 1, Figs. 3 and 4 are sectional views showing the embodiment, and Fig. 5 is a plan view of another plate. , FIGS. 6A and 6B are cross-sectional views taken along lines E-I and Ro-Ro in FIG. 5. FIG. 7 is a plan view of another plate, FIG. FIG. 10 is a sectional view showing a conventional heat exchanger. 2, 32, 42... plate, 4a, 4b...
Rising flange, 5, 35...Bottom wall, 6, 6a,
6b, 36a, 36b, 46a, 46b... opening, 8, 38... opening flange, 9... upper end plate,
15...Lower end plate, 37...Protrusion.

Claims (1)

【特許請求の範囲】 1 底壁の周縁と底壁の中央に設けた中央口の周
縁とに立上りフランジを設け前記中央口と同心の
円上に等分ピツチで偶数個の開口を設け、該開口
の1つおきの周縁に開口フランジを設けてなるプ
レートを、1ピツチずつ円周方向にずらせて重ね
合わせて、前記底壁周縁と中央口周縁のフランジ
をそれぞれ接合するとともに、各開口フランジを
隣接するプレートの開口周縁に接合して、各プレ
ート底壁間に1層おきに連通する第1・第2流路
を形成させ、その上下端面に上端板・下端板を固
着し、第1流路に連通する第1流入口、第1流出
口および第2流路に連通する第2流入口、第2流
出口を上端板、下端板のいずれかに設けてなる熱
交換器の熱交換コア。 2 底壁の外形および中央口が円形をなす特許請
求の範囲第1項記載の熱交換器の熱交換コア。 3 プレートの底壁に複数の突起を設け、該突起
を隣接するピツチ領域内の突起と互に対応しない
位置に配列し、かつ上方または下方のプレートの
底壁に当接させた特許請求の範囲第1項記載の熱
交換器の熱交換コア。 4 前記偶数個の開口を設ける同心円が、複数個
設けられ、各同心円上に同数の開口が設けられた
特許請求の範囲第1項記載の熱交換器の熱交換コ
ア。 5 2個の同心円上に2個ずつの開口が設けら
れ、それら4個の開口が同一直径上に配列され、
かつ2個の開口フランジが互に中心の反対側に配
列された特許請求の範囲第4項記載の熱交換器の
熱交換コア。
[Scope of Claims] 1. A rising flange is provided at the periphery of the bottom wall and a periphery of the central opening provided at the center of the bottom wall, and an even number of openings are provided at equal pitches on a circle concentric with the central opening, and Plates each having an opening flange on the periphery of every other opening are stacked one on top of the other, shifted by one pitch in the circumferential direction, and the flanges on the bottom wall periphery and the center opening periphery are respectively joined, and each opening flange is overlapped. It is joined to the opening periphery of adjacent plates to form first and second channels that communicate every other layer between the bottom walls of each plate, and an upper end plate and a lower end plate are fixed to the upper and lower end surfaces of the first and second flow channels. A heat exchange core of a heat exchanger in which a first inlet and a first outlet communicating with a passage, and a second inlet and a second outlet communicating with a second passage are provided in either an upper end plate or a lower end plate. . 2. The heat exchange core of the heat exchanger according to claim 1, wherein the outer shape of the bottom wall and the central opening are circular. 3 A claim in which a plurality of protrusions are provided on the bottom wall of the plate, the protrusions are arranged in positions that do not correspond to the protrusions in adjacent pitch areas, and are brought into contact with the bottom wall of the upper or lower plate. A heat exchange core of the heat exchanger according to item 1. 4. The heat exchange core of the heat exchanger according to claim 1, wherein a plurality of concentric circles each having an even number of openings are provided, and the same number of openings are provided on each concentric circle. 5 Two openings are provided on two concentric circles, and the four openings are arranged on the same diameter,
A heat exchange core for a heat exchanger according to claim 4, wherein the two open flanges are arranged on opposite sides of the center.
JP6461985A 1985-02-28 1985-03-28 Plate type oil cooler Granted JPS61223213A (en)

Priority Applications (2)

Application Number Priority Date Filing Date Title
JP6461985A JPS61223213A (en) 1985-03-28 1985-03-28 Plate type oil cooler
US06/834,816 US4708199A (en) 1985-02-28 1986-02-28 Heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP6461985A JPS61223213A (en) 1985-03-28 1985-03-28 Plate type oil cooler

Related Child Applications (1)

Application Number Title Priority Date Filing Date
JP22360889A Division JPH02110294A (en) 1989-08-30 1989-08-30 Heat exchanging core for heat exchanger

Publications (2)

Publication Number Publication Date
JPS61223213A JPS61223213A (en) 1986-10-03
JPH0330690B2 true JPH0330690B2 (en) 1991-05-01

Family

ID=13263452

Family Applications (1)

Application Number Title Priority Date Filing Date
JP6461985A Granted JPS61223213A (en) 1985-02-28 1985-03-28 Plate type oil cooler

Country Status (1)

Country Link
JP (1) JPS61223213A (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CA1294605C (en) * 1986-12-31 1992-01-21 Takayuki Ichihara Heat exchanger
JPH064225Y2 (en) * 1987-01-30 1994-02-02 株式会社土屋製作所 Housingless oil cooler
JPS63159675U (en) * 1987-03-31 1988-10-19
JPH0188182U (en) * 1987-11-30 1989-06-09
JPH01106765U (en) * 1987-12-28 1989-07-18
JPH0254060U (en) * 1988-09-30 1990-04-19
JP5511571B2 (en) * 2010-07-29 2014-06-04 三桜工業株式会社 Heat exchanger

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5341820U (en) * 1976-09-14 1978-04-11

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5341820U (en) * 1976-09-14 1978-04-11

Also Published As

Publication number Publication date
JPS61223213A (en) 1986-10-03

Similar Documents

Publication Publication Date Title
JPH073315B2 (en) Heat exchanger
JP3958367B2 (en) Plate heat exchanger
JPH11510890A (en) 3-circuit plate heat exchanger
JP6126358B2 (en) Multi-plate oil cooler
US20110186274A1 (en) Plate heat exchanger
JPS62202997A (en) Heat exchanger of compound type
JP2006183969A (en) Heat-exchange core of stacked oil cooler
JPH0330690B2 (en)
JPH0631694B2 (en) Heat exchanger
JPS5928219Y2 (en) Oil cooler for internal combustion engine
JPH0416710B2 (en)
JP3024653B2 (en) Oil cooler
JPH09184694A (en) Core of laminated type heat exchanger
JPH0461279B2 (en)
JP2597170Y2 (en) Dish-shaped plate for heat exchanger
JPH0443745Y2 (en)
JPH0523981Y2 (en)
JP2509341Y2 (en) Heat exchanger
JPH07190650A (en) Heat exchanger
JP2518495Y2 (en) Combined heat exchanger
JP3024654B2 (en) Oil cooler
JPH0523982Y2 (en)
JPH0356772Y2 (en)
JP7323976B2 (en) Flange structure and heat exchanger with same structure
JP2518521Y2 (en) Heat exchanger

Legal Events

Date Code Title Description
EXPY Cancellation because of completion of term